US2041059A - Method of and apparatus for removing gases from milk or cream or other liquids - Google Patents

Method of and apparatus for removing gases from milk or cream or other liquids Download PDF

Info

Publication number
US2041059A
US2041059A US689452A US68945233A US2041059A US 2041059 A US2041059 A US 2041059A US 689452 A US689452 A US 689452A US 68945233 A US68945233 A US 68945233A US 2041059 A US2041059 A US 2041059A
Authority
US
United States
Prior art keywords
liquid
cream
milk
gases
cones
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US689452A
Inventor
French Thomas Edward
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Aluminium Plant & Vessel Co
ALUMINIUM PLANT and VESSEL Co Ltd
Original Assignee
Aluminium Plant & Vessel Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Aluminium Plant & Vessel Co filed Critical Aluminium Plant & Vessel Co
Application granted granted Critical
Publication of US2041059A publication Critical patent/US2041059A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01JMANUFACTURE OF DAIRY PRODUCTS
    • A01J11/00Apparatus for treating milk
    • A01J11/04Appliances for aerating or de-aerating milk

Definitions

  • this consists in a continuous process for pasteurizing milk or cream or other liquids and disengaging gasestherefrom which consists in causing the liquid to flow successively through a heating device and then as a film with a free surface over a series of moderately inclined surfaces in a closed chamber, successive surfaces having progressively increasing and progressive-- 1y decreasing surface areas curved transversely to the direction of flow of the liquid thereover,
  • the invention also comprises improved apparatus by which the process may be carried out, such apparatus broadly consisting of a chamber containing a plurality of moderately-inclined the angle should not be greater than 45?.
  • the film being subjected to a partial vacuum conical or like surfaces arranged co-axially and base to base in pairs, the alternate upright cones having a central tubular portion at the apex projecting through a larger aperture in the apex of the next upper inverted cone, and an annular space being provided between the outer edges of all the conical surfaces. and the interior wall of the chamber, and means to distribute the liquid on to the uppermost conical surface.
  • a suitable slope of the cones byway of example is that shown in the drawings hereinafter referred to.
  • the liquid is delivered preferably by gravity on to the upper of said surfaces and flows by gravity in thin sheet form with a free upper surface-over the successive surfaces and thereby takes a zig-zag or extended course to a lower discharge outlet or receiver.
  • the apparatus may be such as to provide a liquid receiving chamber below the inclined. or conical surface or surfaces and the inlet and outlet capacities of the apparatus so set or adjustable as to permit the apparatus, whilst operating continuously, to effect short holding and thereby to complete pasteurization partially effected prior to the gas-removing treatment.
  • FIG. 1 isa sectional elevation
  • Fig. 2 a plan view
  • This constructional form of apparatus comprises a closed container I provided at the top with a central inlet 2 for the milk or cream coming from a heat exchanger in which the milk or cream is partially pasteurized.
  • a spreader 3 conveniently in the form of a cup or tray the bottom of which is provided with perforations 4 through which the liquid passes onto the upper part of a conicallsurface formed by a hollow cone 5, down which it then spreads outwardly as a film to the periphery of the cone whence it is shed onto the marginal portion of the inner surface of another hollow cone 6 which is arranged beneath and inverted with respect to the first cone and is medially apertured at 1 so that the liquid film flowing down and contracting towards the centre will fall onto a further cone 8 co-axial with the two cones above it and of similar disposition to the-first cone 6.
  • the inverted cones of the series may be each provided with a rim or peripheral wall 9 extending above the periphery of the adjacent cone above it so that the liquid is prevented from avoiding its proper tortuous path.
  • the liquid after being treated issues from the outlet 9a.
  • the uppermost cone could be an inverted one and the liquid marginally fed to it by an appropriately modified form of spreader.
  • the removal of the gases is assisted by subjecting the film of liquid to the influence of a source of vacuum, and for this purpose an orifice II is provided at the upper end of the container which is adapted to be coupled to means for producing a partial vacuum in the container.
  • the apparatus can be utilized for short holding; which is generally desirable to complete pasteurization, by leaving a sufficient depth below the lowermost cone to provide a chamber In for the liquid to be held in the apparatus for a certain predetermined interval, the time during which the liquid is so held to complete pasteurization being controlled by the depth of the liquid 'in the lower part of the container or the time taken by the liquid to pass through the apparatus, which in turn is dependent on the inlet and outlet capacities of the apparatus. and can be regulated.
  • Steam or a neutral or inert gas may be injected into or blown through the liquid, for instance through a perforated pipe. l2 in the lower part of the container.
  • the capacity of the apparatus may be varied as required by varying the numbers of the cones and the dimensions thereof.
  • Sight-glasses I3 maybe incorporated in the apparatus for inspection purposes.
  • the container may be sealed by a movable cover, or formed of separable sealed-together portions I 4, l5, permitting access to the interior parts, and if desired the cones can be detachably supported in the container.
  • the lowermost cone may be supported on lugs l6 spaced around the inner periphery of the container, the other cones having marginal webs l1 permitting them to rest on each other.
  • the cones that diminish towards the top are provided with a central hollow boss-like extension l8 passing through the substantially wider central apertures 1 in the other cones so that gases escaping from the liquid films on the.inverted cones may have a clear central path through the apparatus to the outlet II at the top of the container, and peripheral space 20 is provided for gases from each of the other cone surfaces to have a clear path of escape to the said outlet and remixing of the evolved gases with the liquids is wholly or mainly avoided.
  • the boss l8 on the uppermost cone may be ported at 2
  • aluminium cones since aluminium if not polished presents a matt surface which promotes the rapid emission of the gases from the liquid sheet.
  • the effect may be enhanced by sand blasting or otherwise roughening the liquid-supporting surfaces.
  • the treated milk or cream withdrawn from the apparatus from the bottom of the container is cooled to the desired final temperature.
  • a continuous process for pasteurizing milk or cream and disengaging gases therefrom during pasteurization which consists in heating the liquid to effect partial pasteurization, then caus-. ing it to flow quietly without further heating as a film with a free surface progressively and a1- ternately increasing and diminishing in extent flowing film to a partial vacuum which is insufficient to cause bubbling of the liquid, then completing the pasteurization of the liquid in the holding chamber, and then without interruption.
  • a continuous process for pasteurizing milk or cream and simultaneously disengaging gases therefrom which consists in heating the liquid to toward a holding chamber'where pasteurizing is completed, and simultaneously subjecting such cooling the liquid effect partial pasteurization, then causing it to fiow quietly without further heating asv a. film with a free surface alternately increasing and diminishing in area over a series of moderately inclined rough surfaces in a closed chamber toward a holding chamber, successive surfaces having progressively increasing and progressively decreasing surface area curved transversely to the direction of the fiow of the film of liquid thereover, and subjecting the flowing film to a partial vacuum which is insuflicient to cause ebullition,
  • a continuous process for pasteurizing milk or cream and disengaging gases therefrom during the pa steurizing process which consists inv heating the liquid to eflect partial pasteurization, then causing it to flow quietly without further heating as a film with a free surface alternately increasing and diminishing in area over a. series of moderately inclined sandblasted surfaces in a closed chamber, successive surfaces having progressively increasing and progressively decreasing surface area curved transversely to the direction of the fiow of the liquid thereover, and subjecting the flowing film of partially pasteurized liquid to a partial vacuum which is insuificient to cause ebullition, then completing the pasteurization of the liquid, and then cooling the liquid withoutinterruption.

Description

May 19, 1936. M T. E. FRENCH 041,059
METHOD OF AND APPARATUS FOR REMOVING GASES FROM MILK OR CREAM OR OTHER LIQUIDS Filed Sept. 14, 1933 2 Sheets-Sheet 1 Fig. 1.
INVEA/ 70R WMQIM May 19, 1936. T. E. FRENCH METHOD OF AND APPARATUS FOR REMOVING GASES FROM MILK 0R CREAM OR .OTHER LIQUIDS 2 Sheets-Sheet 2 Filed Sept. 14, 1933 v INVENTUR Q MZAMJZMA ,mmv /guu JTTORNEYJ Patented May 19, 1936 UNITED STATES PATENT OFFICE METHOD OF AND APPARATUS FORBEMOV- ING GASES FROM MILK OR v OTHER LIQUIDS CREAM OR Thomas Edward French, Kingston, England, assignor to The Aluminium Plant & Vessel Company Limited, London, England Application September 14,1933, Serial No. 689,452 In Great Britain September 30, 1932 3 Claims. (01. 99-212) This can be done by passing the milk oi cream into a vessel where it is subject to a partial vac -uum, various devices being employed for keeping the milk or cream in circulation and for controlling the degree of vacuum, so as to cause ebullition.
Such devices are, in general, complicated and .-expensive, and thepresent invention aims-to provide a novel method of treating the milk or cream or other liquid' to remove the undesired gases and a' simple apparatus for realizing this method.
According to one aspect of the present invention this consists in a continuous process for pasteurizing milk or cream or other liquids and disengaging gasestherefrom which consists in causing the liquid to flow successively through a heating device and then as a film with a free surface over a series of moderately inclined surfaces in a closed chamber, successive surfaces having progressively increasing and progressive-- 1y decreasing surface areas curved transversely to the direction of flow of the liquid thereover,
alternately spreads and contracts and the emisslon of the gases is thereby facilitated. The
surfaces may consist of a succession of gently sloping conical surfaces with the alternate cones inverted with respect to the others, each cone preferably having a matt or roughened surface, for example, an unpolished or sandblasted metal, e. g., aluminium surface, which has the effect of increasing the surface area and the points from which the gases evolve so as further to promote the rapid emissionof the gases. The invention also comprises improved apparatus by which the process may be carried out, such apparatus broadly consisting of a chamber containing a plurality of moderately-inclined the angle should not be greater than 45?.
the film being subjected to a partial vacuum conical or like surfaces arranged co-axially and base to base in pairs, the alternate upright cones having a central tubular portion at the apex projecting through a larger aperture in the apex of the next upper inverted cone, and an annular space being provided between the outer edges of all the conical surfaces. and the interior wall of the chamber, and means to distribute the liquid on to the uppermost conical surface. A suitable slope of the cones byway of example is that shown in the drawings hereinafter referred to. For most purposes an angle between 15 to 30 to the horizontal will serve, but the angle will depend on the viscosity of the liquid and may be less than 15 or higher than 30 in certain cases, although in general working the apparatus, the liquid is delivered preferably by gravity on to the upper of said surfaces and flows by gravity in thin sheet form with a free upper surface-over the successive surfaces and thereby takes a zig-zag or extended course to a lower discharge outlet or receiver.
Theascending gases from the liquid'on the inverted cones rise through the centre of the apparatus the gases ascending from the liquid on the other cones rise through the annular spaces between the outer edges of the cones and the interior wall of the chamber.
The apparatus may be such as to provide a liquid receiving chamber below the inclined. or conical surface or surfaces and the inlet and outlet capacities of the apparatus so set or adjustable as to permit the apparatus, whilst operating continuously, to effect short holding and thereby to complete pasteurization partially effected prior to the gas-removing treatment.
One constructional form of apparatus according to the invention which is well suited for the treatment of milk or cream, is depicted in the accompanying drawings, in which:
,Fig. 1 isa sectional elevation;
Fig. 2 a plan view, and
Fig. 3 is a plan view of a spreader for feeding the liquid to the cones. f
This constructional form of apparatus comprises a closed container I provided at the top with a central inlet 2 for the milk or cream coming from a heat exchanger in which the milk or cream is partially pasteurized. Below the inlet is arranged a spreader 3, conveniently in the form of a cup or tray the bottom of which is provided with perforations 4 through which the liquid passes onto the upper part of a conicallsurface formed by a hollow cone 5, down which it then spreads outwardly as a film to the periphery of the cone whence it is shed onto the marginal portion of the inner surface of another hollow cone 6 which is arranged beneath and inverted with respect to the first cone and is medially apertured at 1 so that the liquid film flowing down and contracting towards the centre will fall onto a further cone 8 co-axial with the two cones above it and of similar disposition to the-first cone 6. Any suitable number of cones so related to each other can be employed. The inverted cones of the series may be each provided with a rim or peripheral wall 9 extending above the periphery of the adjacent cone above it so that the liquid is prevented from avoiding its proper tortuous path. The liquid after being treated issues from the outlet 9a.
Obviously the uppermost cone could be an inverted one and the liquid marginally fed to it by an appropriately modified form of spreader.
The removal of the gases is assisted by subjecting the film of liquid to the influence of a source of vacuum, and for this purpose an orifice II is provided at the upper end of the container which is adapted to be coupled to means for producing a partial vacuum in the container.
- The apparatus can be utilized for short holding; which is generally desirable to complete pasteurization, by leaving a sufficient depth below the lowermost cone to provide a chamber In for the liquid to be held in the apparatus for a certain predetermined interval, the time during which the liquid is so held to complete pasteurization being controlled by the depth of the liquid 'in the lower part of the container or the time taken by the liquid to pass through the apparatus, which in turn is dependent on the inlet and outlet capacities of the apparatus. and can be regulated.
Steam or a neutral or inert gas may be injected into or blown through the liquid, for instance through a perforated pipe. l2 in the lower part of the container.
The capacity of the apparatus may be varied as required by varying the numbers of the cones and the dimensions thereof.
Sight-glasses I3 maybe incorporated in the apparatus for inspection purposes.
The container may be sealed by a movable cover, or formed of separable sealed-together portions I 4, l5, permitting access to the interior parts, and if desired the cones can be detachably supported in the container. For example the lowermost cone may be supported on lugs l6 spaced around the inner periphery of the container, the other cones having marginal webs l1 permitting them to rest on each other.
The cones that diminish towards the top are provided with a central hollow boss-like extension l8 passing through the substantially wider central apertures 1 in the other cones so that gases escaping from the liquid films on the.inverted cones may have a clear central path through the apparatus to the outlet II at the top of the container, and peripheral space 20 is provided for gases from each of the other cone surfaces to have a clear path of escape to the said outlet and remixing of the evolved gases with the liquids is wholly or mainly avoided. The boss l8 on the uppermost cone may be ported at 2| to allow for the lateralescape of the released gases.
It is advantageous to employ aluminium cones since aluminium if not polished presents a matt surface which promotes the rapid emission of the gases from the liquid sheet. The effect may be enhanced by sand blasting or otherwise roughening the liquid-supporting surfaces.
By the. use of conical surfaces inverted with respect to each other the milk or cream is successively spread and contracted.
The treated milk or cream withdrawn from the apparatus from the bottom of the container is cooled to the desired final temperature.
What I 'claim is:-
1. A continuous process for pasteurizing milk or cream and disengaging gases therefrom during pasteurization which consists in heating the liquid to effect partial pasteurization, then caus-. ing it to flow quietly without further heating as a film with a free surface progressively and a1- ternately increasing and diminishing in extent flowing film to a partial vacuum which is insufficient to cause bubbling of the liquid, then completing the pasteurization of the liquid in the holding chamber, and then without interruption.
2. A continuous process for pasteurizing milk or cream and simultaneously disengaging gases therefrom which consists in heating the liquid to toward a holding chamber'where pasteurizing is completed, and simultaneously subjecting such cooling the liquid effect partial pasteurization, then causing it to fiow quietly without further heating asv a. film with a free surface alternately increasing and diminishing in area over a series of moderately inclined rough surfaces in a closed chamber toward a holding chamber, successive surfaces having progressively increasing and progressively decreasing surface area curved transversely to the direction of the fiow of the film of liquid thereover, and subjecting the flowing film to a partial vacuum which is insuflicient to cause ebullition,
then completing pasteurization of th liquid, and then cooling the liquid without interruption.
3'. A continuous process for pasteurizing milk or cream and disengaging gases therefrom during the pa steurizing process which consists inv heating the liquid to eflect partial pasteurization, then causing it to flow quietly without further heating as a film with a free surface alternately increasing and diminishing in area over a. series of moderately inclined sandblasted surfaces in a closed chamber, successive surfaces having progressively increasing and progressively decreasing surface area curved transversely to the direction of the fiow of the liquid thereover, and subjecting the flowing film of partially pasteurized liquid to a partial vacuum which is insuificient to cause ebullition, then completing the pasteurization of the liquid, and then cooling the liquid withoutinterruption.
moms EDWARD FRENCH.
US689452A 1932-09-30 1933-09-14 Method of and apparatus for removing gases from milk or cream or other liquids Expired - Lifetime US2041059A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2041059X 1932-09-30

Publications (1)

Publication Number Publication Date
US2041059A true US2041059A (en) 1936-05-19

Family

ID=10896878

Family Applications (1)

Application Number Title Priority Date Filing Date
US689452A Expired - Lifetime US2041059A (en) 1932-09-30 1933-09-14 Method of and apparatus for removing gases from milk or cream or other liquids

Country Status (1)

Country Link
US (1) US2041059A (en)

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2439260A (en) * 1944-07-26 1948-04-06 Western Condensing Co Apparatus for heating sensitive materials
US2647862A (en) * 1948-09-13 1953-08-04 Phillips Petroleum Co Process and apparatus for vacuum distillation
US2677433A (en) * 1950-11-15 1954-05-04 Kretzschmar Alfred Process and apparatus for degassing boiler feed water
US2684728A (en) * 1952-05-17 1954-07-27 Ind Rayon Corp Apparatus for removing air from viscose solution
US2759883A (en) * 1950-08-15 1956-08-21 Kraft Foods Co Process for deodorization of glyceride oils
US2785765A (en) * 1953-08-03 1957-03-19 Cornell Machine Company Degasser
US2804172A (en) * 1951-07-10 1957-08-27 Sharples Corp Soap deaeration
US2812253A (en) * 1953-03-26 1957-11-05 Apv Co Ltd Treatment of cream
US2944479A (en) * 1956-10-25 1960-07-12 Cherry Burrell Corp Vacuum-steam processor
US3139812A (en) * 1958-05-23 1964-07-07 Heinz Co H J Method of and apparatus for the continuous cooking and sterilization of liquids and suspensions
US3146691A (en) * 1959-10-12 1964-09-01 Martin William Mck Heating device
US3167488A (en) * 1959-11-12 1965-01-26 Malek Jan Michal Solar evaporator
US3226916A (en) * 1963-03-04 1966-01-04 Floyd J Bradford Mud treating apparatus
US3492795A (en) * 1965-08-06 1970-02-03 Lummus Co Separation of vapor fraction and liquid fraction from vapor-liquid mixture
US3503854A (en) * 1967-08-22 1970-03-31 Blaw Knox Co Dual stage steam stripping of vegetable oils at dual pressures
US3516229A (en) * 1967-11-15 1970-06-23 American Cyanamid Co Deaerating apparatus
US3620283A (en) * 1969-02-04 1971-11-16 Artisan Ind Falling film evaporator stripper
US4066540A (en) * 1974-09-12 1978-01-03 Agency Of Industrial Science & Technology Apparatus and method for continuous froth flotation
US4339306A (en) * 1979-10-15 1982-07-13 Voest-Alpine Aktiengesellschaft Apparatus for drying organic material, particularly brown coal
US4352679A (en) * 1981-04-10 1982-10-05 Fmc Corporation Deoxygenating equipment and method of operation
US4358296A (en) * 1981-03-02 1982-11-09 Fmc Corporation Deoxygenating apparatus and method
US6080273A (en) * 1996-07-23 2000-06-27 Schrems; Martin Method and device for treating liquids by partial evaporation
US6482254B1 (en) 2000-11-14 2002-11-19 E. I. Du Pont De Nemours And Company Deaerator insert
US20090229526A1 (en) * 2003-10-13 2009-09-17 Rex Allan Mason Fluid treatment system

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2439260A (en) * 1944-07-26 1948-04-06 Western Condensing Co Apparatus for heating sensitive materials
US2647862A (en) * 1948-09-13 1953-08-04 Phillips Petroleum Co Process and apparatus for vacuum distillation
US2759883A (en) * 1950-08-15 1956-08-21 Kraft Foods Co Process for deodorization of glyceride oils
US2677433A (en) * 1950-11-15 1954-05-04 Kretzschmar Alfred Process and apparatus for degassing boiler feed water
US2804172A (en) * 1951-07-10 1957-08-27 Sharples Corp Soap deaeration
US2684728A (en) * 1952-05-17 1954-07-27 Ind Rayon Corp Apparatus for removing air from viscose solution
US2812253A (en) * 1953-03-26 1957-11-05 Apv Co Ltd Treatment of cream
US2785765A (en) * 1953-08-03 1957-03-19 Cornell Machine Company Degasser
US2944479A (en) * 1956-10-25 1960-07-12 Cherry Burrell Corp Vacuum-steam processor
US3139812A (en) * 1958-05-23 1964-07-07 Heinz Co H J Method of and apparatus for the continuous cooking and sterilization of liquids and suspensions
US3146691A (en) * 1959-10-12 1964-09-01 Martin William Mck Heating device
US3167488A (en) * 1959-11-12 1965-01-26 Malek Jan Michal Solar evaporator
US3226916A (en) * 1963-03-04 1966-01-04 Floyd J Bradford Mud treating apparatus
US3492795A (en) * 1965-08-06 1970-02-03 Lummus Co Separation of vapor fraction and liquid fraction from vapor-liquid mixture
US3503854A (en) * 1967-08-22 1970-03-31 Blaw Knox Co Dual stage steam stripping of vegetable oils at dual pressures
US3516229A (en) * 1967-11-15 1970-06-23 American Cyanamid Co Deaerating apparatus
US3620283A (en) * 1969-02-04 1971-11-16 Artisan Ind Falling film evaporator stripper
US4066540A (en) * 1974-09-12 1978-01-03 Agency Of Industrial Science & Technology Apparatus and method for continuous froth flotation
US4339306A (en) * 1979-10-15 1982-07-13 Voest-Alpine Aktiengesellschaft Apparatus for drying organic material, particularly brown coal
US4358296A (en) * 1981-03-02 1982-11-09 Fmc Corporation Deoxygenating apparatus and method
US4352679A (en) * 1981-04-10 1982-10-05 Fmc Corporation Deoxygenating equipment and method of operation
US6080273A (en) * 1996-07-23 2000-06-27 Schrems; Martin Method and device for treating liquids by partial evaporation
US6482254B1 (en) 2000-11-14 2002-11-19 E. I. Du Pont De Nemours And Company Deaerator insert
AT410903B (en) * 2000-11-14 2003-08-25 Du Pont flow system stability
US20090229526A1 (en) * 2003-10-13 2009-09-17 Rex Allan Mason Fluid treatment system

Similar Documents

Publication Publication Date Title
US2041059A (en) Method of and apparatus for removing gases from milk or cream or other liquids
US2722505A (en) Method of and apparatus for deodorizing oils
GB484117A (en) Improvements in process and apparatus for extraction of oils, fats and other soluble constituents from materials containing the same
US2069714A (en) Pasteurizing apparatus
US1987414A (en) Apparatus for pressure cooking and subsequent cooling of hermetically sealed cans
US2175563A (en) Device for separating oil from water contaminated therewith
US1733324A (en) Process and apparatus for defecating liquid
US2713895A (en) Apparatus for supplying and distributing liquids
US1717927A (en) Evaporator
US2025059A (en) Evaporator
US2220171A (en) Apparatus for the continuous distillation of liquids
HRP920871A2 (en) Apparatus for drying a moist particulate material with superheated steam
US1556230A (en) Coffee-cooling machine
US1648937A (en) Spray-drying apparatus
US2143877A (en) Gas liquid contact apparatus such as distillation apparatus
US831813A (en) Pasteurizing apparatus.
US4929311A (en) Apparatus for deodorizing an organic liquid
US1327599A (en) Apparatus for cooling and scrubbing gases
US831812A (en) Pasteurizing process.
US4929310A (en) Apparatus for deodorizing organic liquids
US1172133A (en) Apparatus for use in the sulfuration of liquids.
US1555432A (en) olier
US2472636A (en) Apparatus for preparing coffee substitutes
US1869008A (en) Process and apparatus for dehydrating oils
US1475639A (en) Air washing and conditioning apparatus